| 학회 |
한국화학공학회 |
| 학술대회 |
2011년 가을 (10/26 ~ 10/28, 송도컨벤시아) |
| 권호 |
17권 2호, p.1750 |
| 발표분야 |
유동층 |
| 제목 |
Modeling a bubbling bed process for CO2 capture from flue gas |
| 초록 |
A model has been developed to investigate effects of important operating parameters on performance of a bubbling-bed adsorber and regenerator system collecting CO2 from flue gas. The particle population balance was considered together with chemical reaction to determine the extent of conversion in both adsorber and regenerator reactors. The calculated CO2 capture efficiency agreed to the measured value reasonably well. Effects of process parameters - temperature, gas velocity, solid circulation rate, moisture content of feed gas - on CO2 capture efficiency have been investigated in a laboratory scale process. The CO2 capture efficiency decreased as temperature or gas velocity increased in the adsorber. However, it increased with moisture content of flue gas fed to the adsorber. |
| 저자 |
최정후1, 김기찬2, 이창근2, 조성호2, 류호정2, 박영철2, 윤필상1
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| 소속 |
1건국대, 2에너지기술(연) |
| 키워드 |
CO2 capture; flue gas; fluidized bed; dual bed; model
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| E-Mail |
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| 원문파일 |
초록 보기 |
